Centrifugal separator and evaporator



c. R. MABEE. CENTRIFUGM. SEPARATOR AND EVAPORATOR.

APPLICATION FILED AUGSSI, \912 1,420,642. Patented June 27, 1922.

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UNl'l'lEil STTS CHARLES R. MABEE, OF CLEVELAND, OHIO.

CENTRIFUGAL SEPARATOR AND EVAPORATOR.

Application filed August 31, 1912.

Be it known that l, @imanes lt. illannn, a citizen of the United States. and resident of Cleveland, in the count)v of Cuyahoga and State of Uhio, have invented certain new and useful Improvements in (lentrifugal Separators and Evaporators, of which l hereby declare the following` to beI a full, clear. and exact description, such as will enable others skilled in the art to which it appertains to make and use the same.

The objects of the invention are to provide. an etlicient easily1 operated and simple form of construction for a machine for removing the water from salt and sugar solutions and from milk and other products, and for evaporatingl purposes generally.

Further objects are to provide a form of machine in which the container for the solution and substances to be affected and the heating surfaces and appliances can be easily cleaned and in which the amount of ,fuel required for heating purposes will he greatly reduced and the fuel can be made more eiiective.

Heretofore vacuum pans and other appliances in use for removing water from solutions of various kinds have required the employment of skilled labor to operate them. The coils of tubing employed for heating the fluids have been enclosed within c vlinders and have been difficult of access for repairs or cleaning. They have been expensive in construction and have required in the several systems a far greater amount el' steam to evaporate a pound of water than is required to produce the same results by means of the improved device hereinafter described.

The present invention has more particular reference to means for applying circumferential movement under centrifugal force of a layer of material or substance containing liquid to evaporate or partially evaporate the liquid therefrom and in Connection therewith, means are provided for heating and for producing a partial vacuum to which the products are exposed, thus causing the evaporation of water from the solutions while in rapid mot-ion, and at the same time constantly eliminating the vapor of evaporation from the solution by mechanical means and subjecting all minute particles of the solution to the reduced atmos- Specification of Letters Patent.

Patented June 27, 1922.

Serial No. 718,114.

pherie pressure by virtue of the constantly changing position of the particles constitutlng the solution.

The vapors and gases thus produced are conveyed out of the machine by means of a vacuum pump with condenser, or by pressure blower or exhaust fan.

he improved machine further comprises a n air tight tube or chamber in which a partial vacuum is maintained and within which the materials to be treated are deposited, means for heating a portion of the tube and means for throwing outwardly the materials against the heating surfaces of the tube and for maintaining them in the form of a thin layer or coating thereon while rapidly moving circumferentially about the inner surface of the tube, and while the vapor of evaporation is mechanically separated from the solution and drawn from the central or axial portion of the tube.

The invention further comprises the combination and arrangement of parts and preferred forms of construction of the various details` as hereinafter described, shown in the accoml)anying drawings and specificalhv pointed out in the claims.

ln the accompanying drawingsI Fig. l is a longitudinal central section of the device: Fig. 2 a transverse section thereof on the line amo. Fig. l; Fig. il is a transverse Section thereof on the line J--o Fig. l Fig. L is an end elevation showing the closure for one end and vacuum gauge; Fig. 5 is a trancverse section of the spider showing a chain operativel \v associated therewith, the chain being' adapted to constitute conveyor means and largely take the place of the rigid con- Jevor means employed in the other embodiment of the invention. i

ln these views A is the cylindrical tube or chamber provided with air tight heads or closures B, B which may be detachable as illustrated to form doors for access to the interior of the. machine. i@ is an exhaust tube communicating with the chamber A through which vapors, gases and other products of evaporation are drawn from the chamber.

The necessary devices for exhausting the vapor of evaporation are made of any suitable. type and hence need not be illustrated, but are operatvelyconnected with the exhaust pipe C,

A steam jacket. D encloses substantially two thirds et the length ot the tube A previding an annular' space D vinto which steam is supplied through a pipe A2. A pressure gauge A3 is also supplied to indicate the steam pressures and a drain cock is also provided as shown at At.

The steam acket is placed nearer one end et the tube A than the other, leaving an unenclosed portion A5 the object ot which will be further described. The exhaust pipe C communicates with this end ot the tube and a tunnel or hopper E controlled by means ot a valve E is employed when introducing material into the tube A tor treatment.

A thermometer T and vacuum gauge G are also shown attached to the other end egt the tube A. A pipe P and valve P are attached to the tube at the loiver right end by means et which a liquid product such as milk is drawn olf trom the tube atter treatment. F, F are spider arms spaced apart, and secured to la shaft F supported in bears ings F2, F2 at each end of the machine. and. rotated atea uniform rate ot speed by means of a pulley F3 or other power operating means.

The outer ends ot the spider arms are connected by means ot suitable appliances for giving a centrifugal movement to the materials to be treated so as to t-hrouY the same against the inner surface ot the heated tube, and to give them a circumferential movement about the inner surtace ot the tube.

The appliances for moving the liquid maj.' be blades F4 F4 as shown in Figs. l. and 3 or they may be flexible appliances such the chains shown in Fig. 5 at F5.

The appliances which produce centrifugal movement in the liquid correspond in length with the length ot the annular steam jacket and coincide in location therewith and the liquid in the unenclosed portion ot the tube is not lifted from the lower portion o t the tube.

The blades F4 F4' are preferably inclined., so as to give an outward centrifugal torce to the fluid in the tube and retain it in close Contact With the interior surface ol' the tube. and the rear surface ot each blade is preterably so designed as to obtain as large an opening as possible in the fluid behind the blade as it revolves, and hence provide an additional area subjected to reduced pressure within the tube.

The manner in which the evaporation and drying of the material enclosed in the tube is obtained may be describen follows and may be illustrated by the treatment ot milk With which the tube is charged. A vacuum of preferably 26 inches is maintained vin the tube Which is that ordinarily employed in upright vacuum pans.

Lesesaal container being properly correlated to the diameter oit the tube and the thickness ot the lilm desired. This iihn absorbs the heat quickly.v 'from the jacket ovfing to the very large heating sur'liace thcrcol". and the rapid passage ot' the layer ot milk thereover.

As the particles oit material under treatnient change their location incessantly they are continuously subjected to the reduced atmospheric pre ire in the interior ot the tube which draws the vapor ot e-,a.jmi'ation away as tast as the vapor `generated by the heat` reduction ol pressure and motion Within the tube.

r)The heavier liquid is separated by the centritugal 'torce trom tie gaseous portions and lies more closely in. contact with the surtace ot the tube. and the gaseous portions are quick y removed through the interior of the tube.

A film ot supcrhcatcd gases will he gencrated between the fluid constituting the layer oit liquid and the sur tace oi the tube and be expelled troni time to time.y greatly accelerating the evaj'lioration ot the Water trom the solution.

`When bodies such as the blades or chains pass rapidly through a liquid they carry ivith them an area oli vapor and leave an open partially vacuous sparc behind them and evaporation is greatly accelerated by this tact.

The chains. When employed. are adapted in the rotary movement thereof. to be torced outwardly into contact with the treating surface ot the container. to the end that said treating surface Will be maintained in a cleansed and polished condition and tree from the adherence ot particles of material such as casein. `when niill is being` treated. l do not, however. herein claim the cleansing devire.y having presented claims to that subject-matter iu my copending applications 40.757, tiled lul'v '19, 191.5, and 77,996, tiled February l2, i916.

The space A which is not enclosed by the steam jacket contains no revolving blades or chains, and hence the liquid is lett comparatively quiet therein so that the vapors and can out ot the exhaust opening Without drawing toom or line particles oli liquid With them.

It is advantageous to convertthe watery portion oli the material which contacts with the heated metal surface at as low a temperature as possible; and it the temperature of such vapor drops a teiv degrees, as it tends to drop immediately on entering the vapor Zone, it is again condensed into globules ot Water. he globules. though tending to be suspendech will, it not immediately drawn out from the vapor-collecting zone, contact again with the layer of material, and again require heating and vaporizing. This watery portion of the solution after the circumferential motions under centrifugal force are maintained for a few minutes collects on the inner surface of the layer where the action of the partial vacuum will have the greatest effect in evaporating and carrying it away, and this will be accomplished much more easily than if the vapor of evaporation were compelled to overcome the weight of. the liquid before it could rise to the surface from the lower portion of an upright vacuum pan.

It has been ascertained by repeated tests that greater efficiency can be secured in the evaporation of fluids by removing the vapor of evaporation in a direction at right angles to the attraction of `gravitation rather than in a direction in opposition to the attraction of gravitation which is the present method in use in vacuum systems.

Then the vapor leaves the surface of a liquid in a vertical direction in the ordinary vacuum pans, where there is a depth of liquid of three or four feet and a considerable distance therefrom to the off take pipe, the upward motion is slow in the fluid and the upward movement against gravity after passing` through the fluid is slow, and a portion of thel vapor condenses into globules and falls back again and it is necessary to reevaporate the same.

In this device the vapor generates from the layer of liquid and is drawn axially and horizontally through the tube and practically at right angles to the attraction of gravity, and hence has far less resistance to overcome from the effects of gravitation, and hence the economy in the use of heat units is greatly promoted.

The speed of evaporation of fluid contained in a vacuum chamber is greatly promoted by the depression below atmospheric pressure. so that water will boil in a vacuum of 26 inches at a temperature of 135 F. The advantage of the phenomena in evaporating and drying milk or other delicate food stuffs is obvious, since the milk will not he chemically changed as would be the case if high temperatures were employed.

In this separating device there is but little adhesion of the milk to the heating surface since the parts are in constant movement and the liquid operated upon is in the form of a layer which passes rapidly over the heating surfaces. For this reason no cooked flavor or odor is imparted to the milk as in the employment of the upright vacuum pans heated from the bottom.

The operation of the conveyor blades is such that the layer of material does not settle but accumulates on the cylindrical surface of the container and has a continuous movement over said surface. A hollow space or quiet zone is maintained within the rim of material into which the heated gases and vapors escape to be taken olf through the exhaust tube C.

It will be appreciated that since the inlet for the material is arranged adjacent one end of the container, whereas the outlet is arranged adjacent the opposite end, the movement of the material while in layer formation, under the action of the conveyor blades is in a direction circumferentially as well as simultaneously endwise towards the discharge end of the container, and assuming that the valve P is open, the treated material will be continuously discharged from the container.

I have in other, co-pending, applications illustrated and described modified forms of evaporating or condensing apparatus, and modified methods of procedure when performing the work of evaporating or con- (lensing.

The application Serial No. 277,904, filed February 18. 1919, has a divisional relation ship with respect to the present application, the claims therein being directed to the method employed.

In application No. 738,178, filed December 23, 1912, I illustrated a mechanism having some features in common with the present one, but also illustrating how the film or layer can. at both of its ends, be sharply defined. as, for example, by extending a wall or abutment radially inward from the container wall.

In application Serial No. 805.598 (division of Serial No. 797,067. renewed as 108,956). filed December 9, 1913, I have shown and described a mechanism of modified form: and in application Serial No. 797,087, filed October 24. 1913, I illustrated and described the method of procedure which is followed in using an apparatus such as shown in said No. 805,598: in this case the material being caused to move axially simultaneously with its circular movements.

In applications No. 40,757, filed July 19, 1915. and No. 77,996, filed February 12, 1916, respectively, I presented a modified mechanism and the method which is followed in employing it, their subjects matter involving film-forming and moving devices which cause the movement of the film or layer circularly and also axially. together with devices for cleansing and polishing the surface of the container. and devices to remove the gases. vapors and air from the central vapor zone, and project such gases and vapors rapidly through a duct by the use of suitable mechanisms.

And I do not herein claim the subjects matter presented by the claims in any of said several co-pending applications.

Having described the invention what I claim as new and desire to se ure by Letters Patent is:

l. In an ei-.faporating apparatus the coinbination of a substantially horizontally disposed closed tubular container' tor the matcrial. to be treated, said container having heated and unheated portions, said container also having an inlet tor the material adjacent one end and an outlet adjacent the opposite end, appliances tor heating a circumferential portion of the container, appliances for producing a partial vacuum therein, and appliances tor giving a circular layer formation to the material in said heated portion and maintaining a circumferential movement ot said layer upon the inner suriiace ot the heated portion oi: the container, said last mentioned appliances being confined to the heated portion only ot the container, whereby a quiet unheated portion for the escape oi vapors is maintained.

2. In. an evaporator, and in combination, a horizontal tube closed at both ends and containing the material lo be treated, eX- ternally applied means Ytor heating the same, said tube having an inlet tor the material at one end, and an outlet adjacent the opposite end, means 't'or producing a partial vacuum therein, ppliances within that portion oi'i' said tube having the outlet tor producing a continuous circumferential mo rement oli a layer of said material within the tube while said layer of material is maintained in contact with the inner surface or' the tube, considerable portion of the tube having the inlet projecting beyond said appliances whereby to maintain a quiet zone at the inlet end of the tube, and means for rotating said appliances.

3. In an. evaporator o'l the character described, the combination of a horizontally disposed cylindrical container closed both ends and having a heated portion and an un.- heated portion, means tor giving a forcible movement to the liquid contained in the heated portion ot said container' to separate vapors ot evaporation trom the substanceunder treatment, the said means serving also to spread the fluid in a thin layer upon the heated portion of the container and to give a continuous circumferential movement to the fluid around the same, the unheated portion of the container being adjacent the inlet end thereof, and said means `terminating with the heated portion, and means tor eX- hausting the vapors in an axial direction from said container through the unheated portion thereof as it is evaporated and separatedv in radial direction 'from the said layer of luid.

4. In an evaporating apparatus, the combination. of a horizontally disposed stationary cylindrical container closed at its ends and having an inlet and outlet tor the material to be treated, means tor regulating the temperature ot the container, conveyor mec ianism arranged. within the container comprising a skeleton drum having a series ot' horizontallyT disposed blades adjacent to but separated from the surface ot the (fontainer, means for rotating said conveyor mechanism at a high speed, the parts being` constructed and arranged whereby a uniiiorin layer olil material is n'iaintained in contact with the surface ot the container while subjected to continuous movement thereover, and means permitting the vapors to escape trom the container.

5, In an evaporating apparatus, the combination or a heated container circular in cross-section, means for regulating the teniperature of the wall thereof, mechanism for supplying the material to be treated, mechanism for forcing the substance outward centritugally towards said wall to form thereon a stratum surrounding au open axial chamber of relatively large diameter, and tor positively moving the stratum circularly over the surface oit said wall, said parts being arranged and operating to force relatively large volumes of vapor inward into said axial chamber, said chamber having a relatively widely expanded escape passage at one end of the layer, and ot cross area approximating the cross area et said chamber adapted to permit said vapor volumes to rapidly escape therethrough.

6. In an evaporating apparatus, the combination of a cylinder having a copious opening at one end, means for regulating the temperature of the wall thereof, means 'tor applying and continuing under movenient a continuous layer or" material to ber treated on and over the cylindrical sur'tace, and ttor maintainingv a central quiet zone within said layer, said cylinder having a copious opening atone end of the said layer for the free escape of vapor and also an opening permitting the discharge ot the treated material independently of the vapors, the area of the discharge opening tor the treated material being relatively small compared to the area of the opening` for the vapor escape, and permitting volumes of vapor to pass out from said Zone relatively much larger than the small stream of material passing through said opening after treatment. i

In testimony whereof, I hereunto set my hand this 22nd day ofAugust, 1912.

' i CHARLES R. MABEE. In presence of- WM. M. MONROE, RALPH BLUE. 

